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JP6066213B2 - Secondary battery manufacturing method and secondary battery - Google Patents
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JP6066213B2 - Secondary battery manufacturing method and secondary battery - Google Patents

Secondary battery manufacturing method and secondary battery Download PDF

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JP6066213B2
JP6066213B2 JP2014052739A JP2014052739A JP6066213B2 JP 6066213 B2 JP6066213 B2 JP 6066213B2 JP 2014052739 A JP2014052739 A JP 2014052739A JP 2014052739 A JP2014052739 A JP 2014052739A JP 6066213 B2 JP6066213 B2 JP 6066213B2
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wound body
pressure
manufacturing
electrolyte
battery case
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JP2015176771A (en
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亮 津久井
亮 津久井
博康 角
博康 角
忍 岡山
忍 岡山
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Toyota Motor Corp
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Priority to KR1020167027955A priority patent/KR101841381B1/en
Priority to PCT/JP2015/001354 priority patent/WO2015136937A1/en
Priority to US15/124,802 priority patent/US10326172B2/en
Priority to CN201580013778.9A priority patent/CN106133951B/en
Priority to EP15717058.0A priority patent/EP3117478B1/en
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/04Construction or manufacture in general
    • H01M10/0431Cells with wound or folded electrodes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/052Li-accumulators
    • H01M10/0525Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/056Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
    • H01M10/0564Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of organic materials only
    • H01M10/0566Liquid materials
    • H01M10/0567Liquid materials characterised by the additives
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/05Accumulators with non-aqueous electrolyte
    • H01M10/058Construction or manufacture
    • H01M10/0587Construction or manufacture of accumulators having only wound construction elements, i.e. wound positive electrodes, wound negative electrodes and wound separators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/4235Safety or regulating additives or arrangements in electrodes, separators or electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/42Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
    • H01M10/44Methods for charging or discharging
    • H01M10/446Initial charging measures
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/60Arrangements or processes for filling or topping-up with liquids; Arrangements or processes for draining liquids from casings
    • H01M50/609Arrangements or processes for filling with liquid, e.g. electrolytes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/60Arrangements or processes for filling or topping-up with liquids; Arrangements or processes for draining liquids from casings
    • H01M50/609Arrangements or processes for filling with liquid, e.g. electrolytes
    • H01M50/627Filling ports
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2300/00Electrolytes
    • H01M2300/0017Non-aqueous electrolytes
    • H01M2300/0025Organic electrolyte
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M50/00Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
    • H01M50/60Arrangements or processes for filling or topping-up with liquids; Arrangements or processes for draining liquids from casings
    • H01M50/609Arrangements or processes for filling with liquid, e.g. electrolytes
    • H01M50/627Filling ports
    • H01M50/636Closing or sealing filling ports, e.g. using lids
    • H01M50/645Plugs
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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  • Chemical & Material Sciences (AREA)
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Description

本発明は、減圧した電池ケース内に電解液を注液する工程を行う二次電池の製造方法および二次電池に関する。   The present invention relates to a secondary battery manufacturing method and a secondary battery that perform a step of injecting an electrolytic solution into a decompressed battery case.

従来から、リチウムイオン二次電池等の二次電池の製造工程では、正極、負極、およびセパレータを捲回してなる捲回体を横向きの姿勢で外装に収納する。
二次電池の製造工程では、外装内に電解液を注液した後で電池容器を密閉し、捲回体に電解液を浸透させる。そして、二次電池の製造工程では、二次電池に対して初期充電を行う。このとき、捲回体には、電解液の分解反応によって皮膜が形成される。
Conventionally, in a manufacturing process of a secondary battery such as a lithium ion secondary battery, a wound body formed by winding a positive electrode, a negative electrode, and a separator is housed in the exterior in a lateral orientation.
In the manufacturing process of the secondary battery, after the electrolyte solution is injected into the exterior, the battery container is sealed, and the electrolyte solution is infiltrated into the wound body. And in the manufacturing process of a secondary battery, initial charge is performed with respect to a secondary battery. At this time, a film is formed on the wound body by the decomposition reaction of the electrolytic solution.

特許文献1に開示される技術では、ケース(電池ケース)の開口部を閉塞してケース内を減圧し、減圧したケース内に電解液を注液する。
特許文献1に開示される技術では、電解液を注液しながら(または、電解液の注液と同時に)、ケース内の圧力を大気圧よりも高い圧力まで上昇させて電解液を捲回体に浸透させている。
In the technique disclosed in Patent Document 1, an opening of a case (battery case) is closed to decompress the inside of the case, and an electrolytic solution is injected into the decompressed case.
In the technique disclosed in Patent Document 1, while injecting an electrolyte solution (or simultaneously with the injection of the electrolyte solution), the pressure in the case is increased to a pressure higher than the atmospheric pressure, and the electrolyte solution is wound. To penetrate.

電解液は、注液直後に毛細管現象によって捲回体の軸方向両端部に浸透する。これにより、捲回体の内側には密閉空間が形成される。
特許文献1に開示される技術のように、電解液を注液しながらケース内の圧力を上昇させた場合には、加圧されたケース内の空気が捲回体の軸方向両端部に浸透した電解液を押しのけて、捲回体内に空気が侵入してしまう可能性がある。
つまり、この場合には、空気の浸入経路および捲回体の軸方向中央部に電解液を浸透させることができない可能性がある。
Immediately after the injection, the electrolytic solution penetrates into both axial ends of the wound body by capillary action. Thereby, a sealed space is formed inside the wound body.
When the pressure in the case is increased while injecting the electrolyte solution as in the technique disclosed in Patent Document 1, the air in the pressurized case penetrates into both axial ends of the wound body. The electrolyte may be pushed away and air may enter the wound body.
That is, in this case, there is a possibility that the electrolytic solution cannot penetrate into the air intrusion path and the axially central portion of the wound body.

このため、特許文献1に開示される技術では、捲回体に均一な皮膜を形成できない可能性がある。   For this reason, with the technique disclosed in Patent Document 1, there is a possibility that a uniform film cannot be formed on the wound body.

特開平9−102443号公報JP-A-9-102443

本発明は、以上の如き状況を鑑みてなされたものであり、捲回体に均一な皮膜を形成できる二次電池の製造方法および二次電池を提供するものである。   The present invention has been made in view of the above situation, and provides a method for manufacturing a secondary battery and a secondary battery that can form a uniform film on a wound body.

本実施形態に係る二次電池の製造方法は、電池ケースと捲回体と電解液とを備える密閉型の二次電池の製造方法であって、前記電池ケースの下面に対して捲回軸方向が平行となるようにして前記捲回体が収納された状態の前記電池ケース内を減圧する工程と、減圧した前記電池ケース内に、分解反応によりガスを発生し得る添加物を添加した電解液を注液する工程と、前記電解液を注液した前記電池ケースを密閉する工程と、密閉した前記電池ケースと捲回体との間の空間である捲回体外部空間と、前記捲回体内部空間との差圧を小さくするために待機して、前記捲回体の軸方向両端部から前記電解液を浸透させて前記捲回体内部空間の体積を減少させる工程と、前記捲回体に前記電解液を浸透させた二次電池を初期充電する工程と、前記電池ケースの密閉を維持しつつ、前記初期充電した前記二次電池を高温エージングする工程と、を行い、前記電解液には、前記添加物の分解反応によるガスの発生によって、前記高温エージングする工程を行うときの前記電池ケース内の圧力が、前記電解液の高温エージング時における飽和蒸気圧以上に高くなる量の添加物が添加される、ものである。 A method for manufacturing a secondary battery according to the present embodiment is a method for manufacturing a sealed secondary battery including a battery case, a wound body, and an electrolyte solution, and a winding axis direction with respect to a lower surface of the battery case A step of decompressing the inside of the battery case in a state where the wound body is accommodated so as to be parallel to each other, and an electrolytic solution in which an additive capable of generating a gas by a decomposition reaction is added to the decompressed battery case A step of sealing the battery case into which the electrolytic solution has been injected, a wound body external space that is a space between the sealed battery case and the wound body, and the wound body Waiting to reduce the differential pressure with the internal space, allowing the electrolytic solution to permeate from both axial ends of the wound body to reduce the volume of the wound body internal space, and the wound body Initially charging a secondary battery infiltrated with the electrolyte solution; A step of performing high temperature aging on the initially charged secondary battery while maintaining sealing of the case, and the step of performing high temperature aging on the electrolyte by generation of gas due to decomposition reaction of the additive. An additive is added in such an amount that the pressure in the battery case when it is performed is higher than the saturated vapor pressure during high-temperature aging of the electrolyte.

本実施形態に係る二次電池の製造方法は、前記電解液には、前記ガスの発生によって、前記高温エージングする工程を行うときの前記電池ケース内の圧力が、前記電解液の高温エージング時における飽和蒸気圧以上に高くなるように量が調整されるとともに、前記初期充電する工程において前記電池ケース内の圧力が前記電解液の高温エージング時における飽和蒸気圧よりも低くなる量の前記添加物が添加される、ものである。   In the method of manufacturing a secondary battery according to the present embodiment, the pressure in the battery case when the high temperature aging process is performed on the electrolytic solution due to the generation of the gas is The amount of the additive is adjusted so as to be higher than the saturated vapor pressure, and the amount of the additive in which the pressure in the battery case is lower than the saturated vapor pressure during high-temperature aging of the electrolytic solution in the initial charging step. It is what is added.

本実施形態に係る二次電池の製造方法は、前記電解液には、前記ガスの発生によって、前記初期充電終了時における前記電池ケース内の圧力が、大気圧と同程度となる量の前記添加物が添加される、ものである。   In the method for manufacturing a secondary battery according to the present embodiment, the electrolyte is added in such an amount that the pressure in the battery case at the end of the initial charging is approximately equal to the atmospheric pressure due to the generation of the gas. Things are added.

本実施形態に係る二次電池の製造方法は、前記初期充電する工程では、前記ガスが発生する電位領域において、他の電位領域よりも低レートで前記二次電池を充電する、ものである。   In the method of manufacturing a secondary battery according to the present embodiment, in the initial charging step, the secondary battery is charged at a lower rate in the potential region where the gas is generated than in other potential regions.

本実施形態に係る二次電池は、電池ケースと、前記電池ケースに収納され捲回体であって前記電池ケースの下面に対して捲回軸方向が平行である捲回体と、電解液と、を具備した密閉型の二次電池である。そして、前記電解液には、分解反応によりガスを発生し得る添加物が添加されており、前記添加物の添加量は、以下の条件:
該添加物の分解反応によるガスの発生によって、高温エージングを行うときの密閉された前記電池ケース内の圧力が、前記電解液の高温エージング時における飽和蒸気圧以上に高くなる
を満たすであることを特徴とする。
Secondary battery according to this embodiment includes a battery case, and the wound body prior Symbol Kaijiku direction winding the lower surface of the battery case a wound body which is housed in the battery case are parallel, electrolytic a liquid, a secondary battery sealed equipped with. Then, before Symbol electrolyte, additives capable of generating gas by decomposition reactions are added, the addition amount of the additives, the following conditions:
By the generation of gas due to the decomposition reaction of the additive, sealed pressure in the battery case when performing Atsushi Ko aging is higher on the saturated vapor pressure at high temperature aging of the electrolyte;
It is the quantity which satisfy | fills .

本発明は、捲回体に均一な皮膜を形成できる、という効果を奏する。   The present invention has an effect that a uniform film can be formed on a wound body.

電池の全体的な構成を示す説明図。Explanatory drawing which shows the whole structure of a battery. 捲回体を製造する様子を示す説明図。(a)正極、負極、およびセパレータを捲回する様子を示す図。(b)捲回体にプレス加工を施す様子を示す図。Explanatory drawing which shows a mode that a winding body is manufactured. (A) The figure which shows a mode that a positive electrode, a negative electrode, and a separator are wound. (B) The figure which shows a mode that press processing is performed to the winding body. 本実施形態の減圧工程から密閉工程までの様子を示す説明図。Explanatory drawing which shows the mode from the pressure reduction process of this embodiment to a sealing process. 注液ユニットを示す説明図。Explanatory drawing which shows an injection unit. 注液ユニットを動作させる様子を示す説明図。(a)減圧工程時の様子を示す図。(b)注液工程時の様子を示す図。Explanatory drawing which shows a mode that a liquid injection unit is operated. (A) The figure which shows the mode at the time of a pressure reduction process. (B) The figure which shows the mode at the time of a liquid injection process. 注液工程時における電解液の浸透度合いを示す説明図。(a)断面図。(b)捲回体の斜視図。Explanatory drawing which shows the osmosis | permeation degree of the electrolyte solution at the time of a liquid injection process. (A) Sectional drawing. (B) The perspective view of a winding body. 本実施形態の浸透工程から高温エージング工程までの様子を示す説明図。Explanatory drawing which shows the mode from the infiltration process of this embodiment to a high temperature aging process. 浸透工程時における電解液の浸透度合いを示す説明図。(a)断面図。(b)捲回体の斜視図。Explanatory drawing which shows the penetration | invasion degree of the electrolyte solution at the time of a osmosis | permeation process. (A) Sectional drawing. (B) The perspective view of a winding body. 初期充電工程時における電解液の浸透度合いを示す説明図。(a)断面図。(b)捲回体の斜視図。Explanatory drawing which shows the osmosis | permeation degree of the electrolyte solution at the time of an initial stage charge process. (A) Sectional drawing. (B) The perspective view of a winding body. 初期充電工程後における電解液の浸透度合いを示す説明図。(a)断面図。(b)捲回体の斜視図。Explanatory drawing which shows the osmosis | permeation degree of the electrolyte solution after an initial stage charge process. (A) Sectional drawing. (B) The perspective view of a winding body. 添加物を変更して皮膜を評価した結果を示す図。The figure which shows the result of having changed the additive and evaluating the film. 電解液に対する添加物としてLPFOを用いた電池と、電解液に対する添加物としてLiBOBを用いた電池とについて、外装内への電解液の注液後から、高温エージング終了時までの外装内圧力の経時変化を示す図。With respect to a battery using LPFO as an additive to the electrolytic solution and a battery using LiBOB as an additive to the electrolytic solution, the aging of the pressure in the exterior from the injection of the electrolytic solution into the exterior to the end of high-temperature aging The figure which shows a change.

以下では、本実施形態の密閉型電池の製造方法(以下、単に「製造方法」と表記する)について説明する。   Below, the manufacturing method (henceforth a "manufacturing method") of the sealed battery of this embodiment is demonstrated.

まず、本発明に係る二次電池の実施形態である電池の概略構成について説明する。   First, a schematic configuration of a battery which is an embodiment of a secondary battery according to the present invention will be described.

本実施形態の電池10は、密閉型のリチウムイオン二次電池である。なお、本発明が適用される対象はリチウムイオン二次電池に限定されるものではなく、ニッケル水素二次電池等の他の二次電池についても適用可能である。   The battery 10 of this embodiment is a sealed lithium ion secondary battery. The target to which the present invention is applied is not limited to the lithium ion secondary battery, but can be applied to other secondary batteries such as a nickel metal hydride secondary battery.

図1に示すように、電池10は、発電要素20、外装30、キャップ40、および外部端子50・50を具備する。   As shown in FIG. 1, the battery 10 includes a power generation element 20, an exterior 30, a cap 40, and external terminals 50 and 50.

発電要素20は、正極101、負極102、およびセパレータ103を捲回してなる捲回体100に電解液Eを浸透させたものである(図2および図3参照)。電池10の充放電時には、発電要素20内で化学反応が起こる(厳密には、正極101と負極102との間で電解液Eを介したイオンの移動が起こる)ことによって電流の流れが発生する。   The power generation element 20 is obtained by infiltrating an electrolyte E into a wound body 100 formed by winding a positive electrode 101, a negative electrode 102, and a separator 103 (see FIGS. 2 and 3). When the battery 10 is charged / discharged, a chemical reaction occurs in the power generation element 20 (strictly speaking, ion movement occurs between the positive electrode 101 and the negative electrode 102 via the electrolytic solution E), thereby generating a current flow. .

電池ケースである外装30は、図1における左右方向を長手方向とする平面視略矩形状に形成される角柱型缶である。外装30は、収納部31と蓋部32とを有する。   The exterior 30 that is a battery case is a prismatic can that is formed in a substantially rectangular shape in plan view with the left-right direction in FIG. 1 as the longitudinal direction. The exterior 30 has a storage part 31 and a lid part 32.

収納部31は、下面および側面が閉塞するとともに、上面が開口した有底角筒状の部材であり、内部に発電要素20を収納する。   The storage unit 31 is a bottomed rectangular tube-shaped member whose bottom surface and side surfaces are closed and whose top surface is open, and stores the power generation element 20 therein.

蓋部32は、収納部31の開口面に応じた形状を有する平板状の部材であり、収納部31の開口面を塞いだ状態で収納部31と接合される。蓋部32において、後述するように外部端子50・50が挿通される箇所の間には、電解液Eを注液するための注液孔33が形成される。   The lid portion 32 is a flat member having a shape corresponding to the opening surface of the storage portion 31 and is joined to the storage portion 31 in a state where the opening surface of the storage portion 31 is closed. In the lid portion 32, a liquid injection hole 33 for injecting the electrolytic solution E is formed between locations where the external terminals 50 and 50 are inserted as will be described later.

注液孔33は、蓋部32の板面を貫通する孔、すなわち、外装30の上面に形成される孔である。注液孔33は、蓋部32の上側(外側)と下側(内側)とで内径寸法が異なる平面視略円状の孔である。注液孔33は、上側の内径が下側の内径よりも大径に形成され、上下中途部に段差部が形成される。   The liquid injection hole 33 is a hole penetrating the plate surface of the lid portion 32, that is, a hole formed in the upper surface of the exterior 30. The liquid injection hole 33 is a substantially circular hole in a plan view having different inner diameters on the upper side (outer side) and the lower side (inner side) of the lid portion 32. The liquid injection hole 33 is formed such that the upper inner diameter is larger than the lower inner diameter, and a step portion is formed in the middle of the upper and lower sides.

キャップ40は、注液孔33を封止する蓋体である。キャップ40の外径は、注液孔33の上側の内径と略同一の寸法となっている。
キャップ40は、注液孔33の前記段差部に載置され、外周縁部がレーザ溶接されることで、蓋部32と接合される。
The cap 40 is a lid that seals the liquid injection hole 33. The outer diameter of the cap 40 is substantially the same as the inner diameter on the upper side of the liquid injection hole 33.
The cap 40 is placed on the step portion of the liquid injection hole 33 and joined to the lid portion 32 by laser welding of the outer peripheral edge portion.

外部端子50・50は、その一部が蓋部32の外側面から電池10の上方(外方)に突出した状態で配置される。外部端子50・50は、集電端子51・51を介して発電要素20の正極101または負極102に電気的に接続される。外部端子50・50は、その外周面部に固定部材34が嵌装されることにより、絶縁部材52・53を間に介して蓋部32に対して絶縁状態で固定される。外部端子50・50および集電端子51・51は、発電要素20に蓄えられる電力を外部に取り出す、若しくは、外部からの電力を発電要素20に取り入れる通電経路として機能する。
集電端子51・51は、発電要素20の正極板、負極板と接続されている。集電端子51・51の材料としては、例えば正極側にアルミニウム、負極側に銅を採用することができる。
The external terminals 50 and 50 are arranged in a state in which part of the external terminals 50 and 50 protrudes upward (outward) of the battery 10 from the outer surface of the lid portion 32. The external terminals 50 and 50 are electrically connected to the positive electrode 101 or the negative electrode 102 of the power generation element 20 through current collecting terminals 51 and 51. The external terminals 50 and 50 are fixed to the lid portion 32 in an insulated state with the insulating members 52 and 53 interposed therebetween by fitting the fixing member 34 on the outer peripheral surface portion thereof. The external terminals 50 and 50 and the current collecting terminals 51 and 51 function as an energization path for taking out the electric power stored in the power generation element 20 to the outside or taking in electric power from the outside into the power generation element 20.
The current collecting terminals 51 and 51 are connected to the positive electrode plate and the negative electrode plate of the power generation element 20. As the material of the current collecting terminals 51 and 51, for example, aluminum can be used on the positive electrode side and copper on the negative electrode side.

外部端子50・50には、電池10の外方側に突出する部位にねじ転造によりねじ加工が施され、ボルト部が形成される。電池10の実使用時には、このボルト部を用いて外部端子50・50にバスバー、外部装置の接続端子等が締結固定される。
締結固定する際、外部端子50・50には締結トルクがかかるとともに、ねじ締結によって軸方向へ外力が付与される。このため、外部端子50・50の材料としては、鉄等の高強度材料を採用することが好ましい。
The external terminals 50 and 50 are threaded by thread rolling at portions protruding outward of the battery 10 to form bolt portions. When the battery 10 is actually used, a bus bar, a connection terminal of an external device, and the like are fastened and fixed to the external terminals 50 and 50 using the bolt portion.
When fastening and fastening, a fastening torque is applied to the external terminals 50 and 50, and an external force is applied in the axial direction by screw fastening. For this reason, it is preferable to employ a high-strength material such as iron as the material of the external terminals 50 and 50.

次に、本実施形態の製造方法について説明する。   Next, the manufacturing method of this embodiment is demonstrated.

まず、製造方法では、ダイコーダ等の塗工機を用いて集電体(正極集電体および負極集電体)の表面に合剤(正極合剤および負極合剤)を塗工した後、合剤を乾燥させる。
次に、製造方法では、集電体の表面上の合剤に対してプレス加工を施すことで、集電体の表面に合剤層(正極合剤層および負極合剤層)を形成して正極101および負極102を生成する。
First, in the manufacturing method, a mixture (a positive electrode mixture and a negative electrode mixture) is applied to the surface of a current collector (a positive electrode current collector and a negative electrode current collector) using a coating machine such as a die coder. Allow the agent to dry.
Next, in the manufacturing method, a mixture layer (a positive electrode mixture layer and a negative electrode mixture layer) is formed on the surface of the current collector by pressing the mixture on the surface of the current collector. A positive electrode 101 and a negative electrode 102 are generated.

図2に示すように、製造方法では、正極101および負極102の間にセパレータ103を挟んで積層する。
製造方法では、正極101の軸方向を捲回軸方向として正極101および負極102の間にセパレータ103を挟んで捲回し、前記捲回したものの外周面に対してプレス加工を施すことで捲回体100を生成する(図2に示す矢印参照)。
As shown in FIG. 2, in the manufacturing method, the separator 103 is sandwiched between the positive electrode 101 and the negative electrode 102 and stacked.
In the manufacturing method, winding is performed by winding the separator 103 between the positive electrode 101 and the negative electrode 102 with the axial direction of the positive electrode 101 as the winding axis direction, and pressing the outer peripheral surface of the wound one. 100 is generated (see arrow shown in FIG. 2).

そして、製造方法では、外装30の蓋部32に一体化された外部端子50・50および集電端子51・51等を捲回体100に接続し、外装30の収納部31に捲回体100を収納する。その後、製造方法では、外装30の収納部31と蓋部32とを溶接によって接合して封缶する。   In the manufacturing method, the external terminals 50 and 50 and the current collecting terminals 51 and 51 integrated with the lid portion 32 of the exterior 30 are connected to the wound body 100, and the wound body 100 is connected to the storage portion 31 of the exterior 30. Storing. Thereafter, in the manufacturing method, the storage portion 31 and the lid portion 32 of the exterior 30 are joined and sealed by welding.

このとき、図2および図3に示すように、製造方法では、捲回体100を横向きの姿勢、すなわち、捲回体100の軸方向(前記捲回軸方向)が外装30の長手方向に対して平行となるように、捲回体100を外装30に収納する。
つまり、図3において、捲回体100の軸方向は、左右方向となる。
At this time, as shown in FIG. 2 and FIG. 3, in the manufacturing method, the winding body 100 is in a lateral orientation, that is, the axial direction of the winding body 100 (the winding axis direction) is relative to the longitudinal direction of the exterior 30. The wound body 100 is housed in the exterior 30 so as to be parallel to each other.
That is, in FIG. 3, the axial direction of the wound body 100 is the left-right direction.

以下では、捲回体100の内部空間、すなわち、正極101、負極102、およびセパレータ103の積層面の間に形成される空間を「捲回体内部空間S1」と表記する。
また、外装30と捲回体100との間の空間、すなわち、外装30の内部空間の中から捲回体内部空間S1を除いた空間を「捲回体外部空間S」と表記する。
Hereinafter, an internal space of the wound body 100, that is, a space formed between the stacked surfaces of the positive electrode 101, the negative electrode 102, and the separator 103 is referred to as a “winding body internal space S1”.
In addition, a space between the exterior 30 and the wound body 100, that is, a space obtained by removing the wound body internal space S <b> 1 from the internal space of the exterior 30 is referred to as “winding body external space S”.

図3に示すように、外装30を封缶した後で、製造方法では、1気圧の大気雰囲気下に配置される外装30内の空気を注液孔33より排出し、外装30内を減圧する減圧工程を行う(図3に示す上向きの矢印A参照)。
このとき、製造方法では、高い真空度となるまで外装30内を減圧する。捲回体内部空間S1の空気は、捲回体100の軸方向両端部100a・100bを通って捲回体外部空間Sに出た後で、外部に排出される。
As shown in FIG. 3, after sealing the exterior 30, in the manufacturing method, the air in the exterior 30 disposed in an atmospheric atmosphere of 1 atm is discharged from the liquid injection hole 33 to reduce the pressure in the exterior 30. A decompression step is performed (see an upward arrow A shown in FIG. 3).
At this time, in the manufacturing method, the inside of the exterior 30 is decompressed until a high degree of vacuum is obtained. The air in the wound body internal space S1 passes through both end portions 100a and 100b in the axial direction of the wound body 100 and exits to the wound body outer space S, and is then discharged to the outside.

外装30内を減圧した後で、製造方法では、注液孔33より減圧した外装30内に電解液Eを注液する注液工程を行う(図3に示す矢印E参照)。   After reducing the pressure inside the exterior 30, in the manufacturing method, a liquid injection step of injecting the electrolytic solution E into the external pressure 30 from the liquid injection hole 33 is performed (see arrow E shown in FIG. 3).

このような減圧工程および注液工程は、例えば、図4に示すような注液ユニット110を用いて行われる。   Such a pressure reduction process and a liquid injection process are performed using the liquid injection unit 110 as shown in FIG. 4, for example.

図4に示すように、注液ユニット110は、内部に電解液Eが貯溜される注液ポッド111が三方弁112の上側のポートに接続されるとともに、真空ポンプが三方弁112の左側のポートに接続されるものである。
注液ユニット110は、外装30の上方に配置され、上下方向に移動可能、すなわち、昇降可能に構成される。図4において、三方弁112の下側のポートには、他の部材が接続されていない状態である。
As shown in FIG. 4, the liquid injection unit 110 includes a liquid injection pod 111 in which an electrolytic solution E is stored, connected to the upper port of the three-way valve 112, and a vacuum pump connected to the left port of the three-way valve 112. Is connected to.
The liquid injection unit 110 is disposed above the exterior 30 and is configured to be movable in the vertical direction, that is, to be able to move up and down. In FIG. 4, the other port is not connected to the lower port of the three-way valve 112.

図5(a)に示すように、製造方法では、減圧工程を行うときに、注液ユニット110を下降させて、三方弁112と注液孔33の段差部とを接触させて注液孔33をシールし、外装30を三方弁112の下側のポートに接続する。
そして、製造方法では、三方弁112を制御して外装30と真空ポンプとを連通し、真空ポンプを駆動させて外装30内を減圧する。
As shown in FIG. 5A, in the manufacturing method, when the pressure reducing process is performed, the liquid injection unit 110 is lowered to bring the three-way valve 112 and the step portion of the liquid injection hole 33 into contact with each other, thereby injecting the liquid injection hole 33. And the exterior 30 is connected to the lower port of the three-way valve 112.
In the manufacturing method, the three-way valve 112 is controlled to connect the exterior 30 and the vacuum pump, and the vacuum pump is driven to decompress the interior of the exterior 30.

図5(b)に示すように、外装30を減圧した後で、製造方法では、三方弁112を制御して外装30と注液ポッド111とを連通し、外装30内の圧力と真空ポッド内の圧力との差圧を利用して外装30内に電解液Eを注液する。   As shown in FIG. 5 (b), after the exterior 30 is depressurized, in the manufacturing method, the three-way valve 112 is controlled so that the exterior 30 and the liquid injection pod 111 communicate with each other. The electrolytic solution E is injected into the exterior 30 using a pressure difference from the above pressure.

このとき、図6に示すように、電解液Eは、毛細管現象によって、注液直後に捲回体100の軸方向両端部100a・100bに勢いよく浸透する(図6に示す矢印参照)。
これにより、捲回体100の軸方向両端部100a・100bには、電解液Eが浸透し、電解液Eによって正極101、負極102、およびセパレータ103の積層面の間に形成される空間が埋められる。
At this time, as shown in FIG. 6, the electrolyte E penetrates vigorously into the axial end portions 100 a and 100 b of the wound body 100 immediately after the injection due to capillary action (see arrows shown in FIG. 6).
As a result, the electrolyte solution E permeates the axial end portions 100a and 100b of the wound body 100, and the electrolyte solution E fills the space formed between the stacked surfaces of the positive electrode 101, the negative electrode 102, and the separator 103. It is done.

つまり、捲回体内部空間S1は、注液直後に電解液Eによって捲回体外部空間Sから隔絶されて密閉空間となる。
捲回体内部空間S1が密閉空間となった時点において、捲回体外部空間Sおよび捲回体内部空間S1は、大気圧よりも十分に圧力が低い空間、すなわち、真空層となっている。
That is, the wound body internal space S1 is isolated from the wound body external space S by the electrolytic solution E immediately after the injection, and becomes a sealed space.
When the wound body inner space S1 becomes a sealed space, the wound body outer space S and the wound body inner space S1 are spaces whose pressure is sufficiently lower than the atmospheric pressure, that is, a vacuum layer.

本実施形態の製造方法では、リチウム塩を有機溶媒等に溶解させたものに、添加物を添加したものを、電解液Eとして用いている。
リチウム塩としては、例えば、LiPF6(ヘキサフルオロリン酸リチウム)等がある。
有機溶剤としては、例えば、エチレンカーボネート等がある。
In the manufacturing method of the present embodiment, a solution obtained by adding an additive to a solution obtained by dissolving a lithium salt in an organic solvent or the like is used as the electrolytic solution E.
Examples of the lithium salt include LiPF6 (lithium hexafluorophosphate).
Examples of the organic solvent include ethylene carbonate.

本実施形態の製造方法では、以下の構造式に示す物質を、添加物として添加している。

Figure 0006066213
In the manufacturing method of this embodiment, the substance shown in the following structural formula is added as an additive.
Figure 0006066213

なお、以下においては、前記構造式1に示す物質を「添加物LPFO」と表記する。   In the following, the substance represented by the structural formula 1 is referred to as “additive LPFO”.

このように、本実施形態の製造方法では、注液工程で添加物LPFOを添加した電解液Eを外装30内に注液する。   Thus, in the manufacturing method of the present embodiment, the electrolytic solution E to which the additive LPFO has been added in the liquid injection step is injected into the exterior 30.

図3に示すように、電解液Eを外装30内に注液した後で、製造方法では、外装30内を大気圧(本実施形態では1気圧)に戻す(図3に示す下向きの矢印A参照)。
このとき、製造方法では、図6(a)に示す状態から注液ユニット110を上昇させ、外装30を大気開放する。これにより、製造方法では、捲回体外部空間Sを大気圧に戻す。
As shown in FIG. 3, after injecting the electrolyte E into the exterior 30, the manufacturing method returns the interior of the exterior 30 to atmospheric pressure (1 atmosphere in the present embodiment) (downward arrow A shown in FIG. 3). reference).
At this time, in the manufacturing method, the liquid injection unit 110 is raised from the state shown in FIG. Thereby, in the manufacturing method, the wound body outer space S is returned to atmospheric pressure.

大気圧に戻した捲回体外部空間Sと捲回体内部空間S1との差圧は、最大でも1気圧程度、つまり、小さいものとなる。
従って、大気開放時に外装30(捲回体外部空間S)に導入される空気は、捲回体100の軸方向両端部100a・100bに浸透した電解液Eを押しのけることができない。
The differential pressure between the wound body outer space S and the wound body inner space S1 returned to the atmospheric pressure is about 1 atm at most, that is, small.
Therefore, the air introduced into the exterior 30 (winding body outer space S) when the atmosphere is released cannot push out the electrolytic solution E that has permeated the axial end portions 100a and 100b of the winding body 100.

このため、捲回体内部空間S1は、外装30を大気開放した後も、捲回体外部空間Sから隔絶されたままの状態、すなわち、減圧されたままの状態(真空層が形成されている状態)である。   For this reason, the wound body inner space S1 remains isolated from the wound body outer space S even after the exterior 30 is opened to the atmosphere, that is, in a state where the wound body is decompressed (a vacuum layer is formed). State).

なお、製造方法では、注液工程後も捲回体内部空間が捲回体外部空間から隔絶されたままの状態を維持できる程度に、捲回体外部空間の圧力を捲回体内部空間の圧力よりも高くすればよく、必ずしも注液工程後に捲回体外部空間を大気圧に戻す必要はない。
例えば、製造方法は、注液工程後に、捲回体内部空間を大気圧よりも数Pa程度高い圧力、または数Pa程度低い圧力まで加圧しても構わない。
In the manufacturing method, the pressure of the wound body external space is adjusted so that the wound body internal space can be kept isolated from the wound body external space even after the liquid injection process. It is not necessary to return the outer space of the wound body to atmospheric pressure after the liquid injection process.
For example, the manufacturing method may pressurize the inner space of the wound body to a pressure higher by several Pa than atmospheric pressure or a pressure lower by several Pa after the liquid injection process.

外装30内を大気圧に戻した後で、製造方法では、キャップ40を注液孔33に載置して、レーザ溶接機によってキャップ40の外縁部に沿ってレーザを照射し、注液孔33を本封止する(図3に示す黒塗りの三角形参照)。
このように、製造方法では、キャップ40を注液孔33に溶接し、キャップ40によって注液孔33を本封止して、電解液Eを注液した外装30を密閉する密閉工程を行う。
After the interior of the exterior 30 is returned to atmospheric pressure, in the manufacturing method, the cap 40 is placed in the liquid injection hole 33, and laser is irradiated along the outer edge of the cap 40 by a laser welding machine. Is sealed (see the black triangle shown in FIG. 3).
Thus, in the manufacturing method, the cap 40 is welded to the liquid injection hole 33, the liquid injection hole 33 is fully sealed by the cap 40, and the sealing process for sealing the exterior 30 in which the electrolytic solution E is injected is performed.

これにより、捲回体外部空間Sは、密閉空間となる。このとき、捲回体外部空間Sの圧力は、大気圧となっている。   Thereby, the wound body external space S becomes a sealed space. At this time, the pressure in the wound body outer space S is atmospheric pressure.

図7に示すように、密閉工程を行った後で、製造方法では、外装30を一定時間放置して捲回体100に電解液Eを浸透させる浸透工程を行う(図7の左上に示す外装30参照)。   As shown in FIG. 7, after the sealing process is performed, in the manufacturing method, the exterior 30 is left for a certain period of time to perform a permeation process in which the electrolytic solution E penetrates into the wound body 100 (the exterior shown in the upper left of FIG. 7). 30).

製造方法では、浸透工程前(捲回体100の軸方向両端部100a・100bに電解液Eを浸透させた後)に密閉工程を行うことで、浸透工程時に外部から外装30内に空気が浸入することを防止している。
これにより、製造方法は、電解液Eの蒸発や空気に含まれる水分および酸素の影響に起因する電池性能の低下を抑制できる。
In the manufacturing method, air enters the exterior 30 from the outside during the permeation process by performing a sealing process before the permeation process (after the electrolyte E has permeated the axial ends 100a and 100b of the wound body 100). To prevent it.
Thereby, the manufacturing method can suppress the fall of the battery performance resulting from the evaporation of the electrolyte solution E and the influence of the water | moisture content and oxygen contained in air.

密閉工程および浸透工程を行うとき、捲回体外部空間Sの圧力は大気圧である。一方、捲回体内部空間S1の圧力は、高い真空度すなわち、真空に近い圧力である。   When performing the sealing step and the infiltration step, the pressure in the wound body outer space S is atmospheric pressure. On the other hand, the pressure in the winding body internal space S1 is a high degree of vacuum, that is, a pressure close to vacuum.

つまり、製造方法では、捲回体外部空間Sの圧力が捲回体内部空間S1の圧力よりも高い状態で、密閉工程および浸透工程を行う。
これにより、図8に示すように、製造方法では、捲回体外部空間Sと捲回体内部空間S1との差圧を埋めるように、捲回体100に電解液Eを浸透させる。
That is, in the manufacturing method, the sealing step and the infiltration step are performed in a state where the pressure in the wound body outer space S is higher than the pressure in the wound body inner space S1.
Thereby, as shown in FIG. 8, in the manufacturing method, the electrolytic solution E is infiltrated into the wound body 100 so as to fill the differential pressure between the wound body outer space S and the wound body inner space S1.

具体的には、電解液Eの浸透に伴って電解液Eの液面の高さ位置が下がるため、捲回体外部空間Sの体積は大きくなる。
従って、密閉工程後の捲回体外部空間Sの圧力は、電解液Eの浸透に伴って低くなる。
Specifically, since the height position of the liquid surface of the electrolytic solution E is lowered as the electrolytic solution E penetrates, the volume of the wound body outer space S is increased.
Therefore, the pressure in the wound body outer space S after the sealing step becomes lower as the electrolyte E penetrates.

電解液Eは、軸方向両端部100a・100bから軸方向中央部100cに向けて浸透するとともに、捲回体内部空間S1(真空層)を、捲回体100の軸方向中央部100cに向けて移動させる(図8(a)に示す矢印参照)。
従って、捲回体内部空間S1の体積は、電解液Eの浸透に伴って小さくなる。このため、捲回体内部空間S1の圧力は、電解液Eの浸透に伴って高くなる。
The electrolyte E penetrates from the axial end portions 100a and 100b toward the axial center portion 100c, and the winding body internal space S1 (vacuum layer) is directed toward the axial center portion 100c of the winding body 100. Move (see arrow shown in FIG. 8A).
Therefore, the volume of the wound body internal space S1 decreases as the electrolyte E penetrates. For this reason, the pressure in the winding body internal space S1 increases as the electrolyte E penetrates.

つまり、製造方法では、電解液Eの浸透に伴って圧力が低くなる捲回体外部空間Sの圧力を、電解液Eの浸透に伴って圧力が高くなる捲回体内部空間S1の圧力よりも高くしておくことで、電解液Eの浸透によって捲回体外部空間Sと捲回体内部空間S1との差圧が小さくなるようにしている。   That is, in the manufacturing method, the pressure in the wound body outer space S, where the pressure decreases as the electrolyte solution E penetrates, is greater than the pressure in the wound body internal space S1, where the pressure increases as the electrolyte solution E penetrates. By making it high, the differential pressure between the wound body outer space S and the wound body inner space S1 is reduced by the permeation of the electrolytic solution E.

これによれば、製造方法は、捲回体外部空間Sと捲回体内部空間S1との差圧を利用して、捲回体100に電解液Eを効果的に浸透させることができる。
従って、製造方法は、電解液Eの捲回体100への浸透を促進できる。
According to this, the manufacturing method can make the electrolyte solution E permeate | transmit the winding body 100 effectively using the differential pressure | voltage of the winding body outer space S and the winding body internal space S1.
Therefore, the manufacturing method can promote the penetration of the electrolytic solution E into the wound body 100.

このように、浸透工程では、外装30の密閉状態を維持して、密閉した外装30の捲回体外部空間Sと、捲回体内部空間S1との差圧を小さくするために待機して、捲回体100の軸方向両端部100a・100bから電解液Eを浸透させて捲回体内部空間S1の体積を減少させる。
また、捲回体100は、密閉工程後に放置されることで、軸方向両端部100a・100bから電解液Eが浸透して捲回体内部空間S1の体積が減少される。
Thus, in the permeation step, while maintaining the sealed state of the exterior 30 and waiting to reduce the differential pressure between the wound body outer space S of the sealed exterior 30 and the wound body inner space S1, The electrolytic solution E is infiltrated from both ends 100a and 100b in the axial direction of the wound body 100 to reduce the volume of the wound body internal space S1.
Further, the wound body 100 is left after the sealing step, so that the electrolyte E penetrates from both axial ends 100a and 100b, and the volume of the wound body internal space S1 is reduced.

電解液Eは、捲回体外部空間Sと捲回体内部空間S1との差圧が大きいほど、速い速度で捲回体100に浸透する。このため、電解液Eは、密閉工程直後において、捲回体100に勢いよく浸透する。
電解液Eの浸透に伴って、捲回体外部空間Sと捲回体内部空間S1との差圧が小さくなるため、電解液Eは、時間の経過とともに捲回体100に浸透する速度が遅くなる。
そして、電解液Eは、捲回体外部空間Sと捲回体内部空間S1との圧力が平衡になったとき(釣り合ったとき)に、捲回体100への浸透が停止する。
The electrolytic solution E penetrates the wound body 100 at a higher speed as the differential pressure between the wound body outer space S and the wound body inner space S1 is larger. For this reason, the electrolyte solution E penetrates the wound body 100 vigorously immediately after the sealing step.
As the electrolytic solution E penetrates, the differential pressure between the wound body outer space S and the wound body inner space S1 becomes smaller, so that the speed of the electrolyte E penetrating into the wound body 100 with time elapses. Become.
The electrolyte E stops permeating the wound body 100 when the pressures in the wound body outer space S and the wound body inner space S1 are balanced (when balanced).

そこで、本実施形態の浸透工程では、捲回体外部空間Sと捲回体内部空間S1との圧力が平衡になるまで待機する。
このような浸透工程における待機時間は、例えば、外装30内、すなわち、捲回体外部空間Sの圧力を市販の圧力センサで測定し、前記圧力センサの測定結果が一定となるまでの時間を評価した結果等に基づいて適宜設定される。
Therefore, in the infiltration process of the present embodiment, the process waits until the pressures in the wound body outer space S and the wound body inner space S1 are balanced.
The waiting time in such an infiltration step is, for example, measuring the pressure in the exterior 30, that is, the pressure in the wound body outer space S with a commercially available pressure sensor, and evaluating the time until the measurement result of the pressure sensor becomes constant. It is set as appropriate based on the results.

ここで、捲回体100は、厚み方向両側面と収納部31の短手方向両側面との間に僅かな隙間が形成された状態、若しくは、厚み方向両側面と収納部31の短手方向両側面とが密着した状態で、外装30に収納される。   Here, the wound body 100 is in a state where a slight gap is formed between both side surfaces in the thickness direction and both side surfaces in the short direction of the storage unit 31 or in the short direction of both side surfaces in the thickness direction and the storage unit 31. It is accommodated in the exterior 30 in a state where both side surfaces are in close contact.

従って、捲回体外部空間Sは、電解液Eを注液する前の状態において、捲回体100の上下両側方と左右両側方の空間が、その体積の大部分を占めている。
また、外装30内に電解液Eが注液されることにより、捲回体外部空間Sの体積は、例えば、半分程度まで小さくなる。
Therefore, in the state before the wound body outer space S is injected with the electrolytic solution E, the space on both the upper and lower sides and the left and right sides of the wound body 100 occupies most of the volume.
Further, when the electrolytic solution E is injected into the exterior 30, the volume of the wound body outer space S is reduced to, for example, about half.

つまり、捲回体外部空間Sは、浸透工程を開始した時点における体積が小さいため、電解液Eの浸透に伴って圧力が低くなり易い。
従って、捲回体外部空間Sと捲回体内部空間S1との圧力が平衡になるまで待機した場合でも、電解液Eは、捲回体100の軸方向中央部100cまで浸透しない。
That is, since the volume of the wound body outer space S is small at the time of starting the permeation process, the pressure tends to decrease with the permeation of the electrolytic solution E.
Accordingly, even when waiting for the pressure in the wound body outer space S and the wound body inner space S1 to be balanced, the electrolyte E does not penetrate to the axially central portion 100c of the wound body 100.

図7および図9に示すように、浸透工程を行った後で、製造方法では、捲回体100に電解液Eを浸透させた電池10を初期充電する初期充電工程を行う。   As shown in FIG. 7 and FIG. 9, after the infiltration step is performed, in the manufacturing method, an initial charging step for initially charging the battery 10 in which the electrolytic solution E is infiltrated into the wound body 100 is performed.

このとき、製造方法では、外装30の密閉状態を維持しつつ、外装30を拘束治具によって拘束し、外装30の厚み方向(図7における紙面奥行き方向)に沿って、外装30に対して所定の大きさの荷重を付与する。
そして、製造方法では、電源装置120の電極を外部端子50・50に接続し、電池10を初期充電する。
At this time, in the manufacturing method, while maintaining the sealed state of the exterior 30, the exterior 30 is restrained by a restraining jig, and is predetermined with respect to the exterior 30 along the thickness direction of the exterior 30 (the depth direction in FIG. 7). The load of the magnitude | size of is given.
And in a manufacturing method, the electrode of the power supply device 120 is connected to the external terminals 50 and 50, and the battery 10 is initially charged.

これにより、捲回体100には、電解液Eが浸透している部分で添加物LPFO(電解液E)が分解反応を起こし、電解液Eが浸透している部分に皮膜が形成される。   Thereby, in the wound body 100, the additive LPFO (electrolytic solution E) causes a decomposition reaction at a portion where the electrolytic solution E penetrates, and a film is formed at a portion where the electrolytic solution E penetrates.

このとき、捲回体100は、軸方向両端部100a・100bから皮膜が形成される(図9に白塗りで示す矢印参照)。   At this time, the wound body 100 is formed with a film from both axial end portions 100a and 100b (see arrows shown in white in FIG. 9).

また、捲回体100の皮膜が形成された部分においては、皮膜形成の分解反応を除く添加物LPFO(電解液E)の分解反応によってガスGが発生する。
つまり、初期充電工程では、捲回体内部空間S1の外側でガスGが発生する。
Further, in the portion of the wound body 100 where the film is formed, gas G is generated by the decomposition reaction of the additive LPFO (electrolytic solution E) excluding the decomposition reaction for film formation.
That is, in the initial charging step, gas G is generated outside the wound body internal space S1.

このように、製造方法では、電解液Eに添加物LPFOを添加することで、皮膜形成時に意図的にガスGを発生させ、捲回体内部空間S1とその外側の空間(より詳細には、捲回体100の皮膜が形成された部分)とに差圧を生み出しているのである。   Thus, in the manufacturing method, by adding the additive LPFO to the electrolytic solution E, the gas G is intentionally generated at the time of film formation, and the wound body inner space S1 and the outer space (more specifically, A differential pressure is generated between the wound body 100 and the portion on which the film is formed.

このため、製造方法では、初期充電工程を行うときにも、捲回体100に電解液Eを浸透させることができる(図9の捲回体100の軸方向中央部100c近傍に示す矢印参照)。   For this reason, in the manufacturing method, the electrolytic solution E can be infiltrated into the wound body 100 even when the initial charging step is performed (see the arrow shown in the vicinity of the axial center portion 100c of the wound body 100 in FIG. 9). .

具体的には、捲回体100における、捲回体内部空間S1の外側に位置する電解液Eが浸透している部分にガスGが発生すると気泡となり、その場にとどまる。電解液Eが浸透している部分にとどまった気泡により、電解液Eが捲回体100の軸方向中央部100c、および捲回体100の外部へ向けて押し出される。
これにより、電解液Eは捲回体100の軸方向中央部100cに浸透していく。また、捲回体100の外部へ押し出された電解液Eは、捲回体100外部に存在する電解液Eから発生した気泡によって捲回体内部空間S1よりも陽圧となった捲回体外部空間Sの圧力により、再び捲回体100内に押し込まれる。
このように、初期充電工程においては、発生したガスGにより捲回体100に電解液Eが浸透されることとなる。
Specifically, when the gas G is generated in a portion of the wound body 100 where the electrolytic solution E located outside the wound body internal space S1 is permeated, bubbles are formed and remain there. Due to the bubbles remaining in the portion where the electrolytic solution E has permeated, the electrolytic solution E is pushed out toward the axially central portion 100c of the wound body 100 and the outside of the wound body 100.
As a result, the electrolytic solution E penetrates into the axially central portion 100c of the wound body 100. In addition, the electrolyte E pushed out of the wound body 100 is outside the wound body in which the pressure generated by the air bubbles generated from the electrolyte E existing outside the wound body 100 is higher than that of the wound body internal space S1. It is pushed into the wound body 100 again by the pressure in the space S.
Thus, in the initial charging step, the electrolytic solution E is infiltrated into the wound body 100 by the generated gas G.

従って、製造方法は、電解液Eを捲回体100の軸方向中央部100cに向けてさらに浸透させることができるとともに、捲回体内部空間S1(真空層)を、捲回体100の軸方向中央部100cに圧縮することができる(図9の軸方向中央部100c近傍に示す矢印参照)。   Therefore, in the manufacturing method, the electrolytic solution E can be further permeated toward the axially central portion 100c of the wound body 100, and the wound body internal space S1 (vacuum layer) can be formed in the axial direction of the wound body 100. The center portion 100c can be compressed (see the arrow in the vicinity of the central portion 100c in the axial direction in FIG. 9).

つまり、製造方法では、初期充電工程において、捲回体100の浸透工程で電解液Eを浸透させた部分に皮膜を形成するとともに、皮膜形成時に発生するガスGを利用して浸透工程で浸透させることができなかった部分に電解液Eを浸透させる(図9に示す矢印参照)。   That is, in the manufacturing method, in the initial charging process, a film is formed on the portion where the electrolyte solution E is infiltrated in the infiltration process of the wound body 100, and the gas G generated during the film formation is used to infiltrate in the infiltration process. The electrolyte solution E is infiltrated into the portion that could not be obtained (see the arrow shown in FIG. 9).

これにより、図10に示すように、製造方法は、初期充電工程中に捲回体100の軸方向中央部100cまで電解液Eを浸透させることができる。つまり、製造方法は、捲回体100の全面に電解液Eを浸透させることができる。
また、製造方法は、浸透工程で電解液Eを浸透させることができた部分(捲回体100の軸方向中央部100cを除く部分)に皮膜を形成後、初期充電工程中に電解液Eを浸透させることができた部分(軸方向中央部100c)に皮膜を形成できる。
Thereby, as shown in FIG. 10, the manufacturing method can permeate | transmit the electrolyte solution E to the axial direction center part 100c of the winding body 100 during an initial stage charging process. That is, in the manufacturing method, the electrolytic solution E can penetrate the entire surface of the wound body 100.
In addition, the manufacturing method includes forming a film on a portion where the electrolytic solution E can be permeated in the permeation step (a portion excluding the central portion 100c in the axial direction of the wound body 100), and then applying the electrolytic solution E during the initial charging step. A film can be formed on the portion (the axially central portion 100c) that could be permeated.

これによれば、製造方法は、捲回体100の軸方向両端部100a・100bから軸方向中央部100cに向けて順次皮膜を形成できる。また、製造方法は、皮膜が形成された部分において、ガスGを意図的に発生させることで必要以上(皮膜形成後)に電解液Eと活物質とが接触してしまうことを防止できる。
従って、製造方法は、浸透工程で電解液Eを浸透させることができた部分に過剰に皮膜が形成されてしまうことを防止できる。
According to this, a manufacturing method can form a membrane | film | coat sequentially from the axial direction both ends 100a * 100b of the winding body 100 toward the axial direction center part 100c. Moreover, the manufacturing method can prevent the electrolyte solution E and an active material from contacting more than necessary (after film formation) by intentionally generating gas G in the part in which the film was formed.
Therefore, the manufacturing method can prevent the film from being excessively formed in the portion where the electrolytic solution E could be permeated in the permeation step.

つまり、製造方法は、捲回体100の全面に均一な皮膜を形成できる。
このため、製造方法では、ポテンシャルを最大限引き出すことが可能な電池10を製造できる。
That is, the manufacturing method can form a uniform film on the entire surface of the wound body 100.
For this reason, in the manufacturing method, the battery 10 capable of maximizing the potential can be manufactured.

また、製造方法は、初期充電工程時に電解液Eを捲回体100の軸方向中央部100cに浸透させることで、軸方向中央部100c、すなわち、真空層を圧縮できる。
従って、製造方法は、放熱性の良好な電池10を製造できる。
Moreover, the manufacturing method can compress the axial direction center part 100c, ie, a vacuum layer, by making electrolyte solution E permeate | transmit the axial direction center part 100c of the winding body 100 at the time of an initial charging process.
Therefore, the manufacturing method can manufacture the battery 10 with good heat dissipation.

ここで、電解液Eは、ガスGが発生した分と同程度、すなわち、ガスGの体積分と同程度の量だけ捲回体100の軸方向中央部100cに浸透する。
例えば、初期充電工程時に約3ccのガスGが発生した場合、電解液Eは、約3cc分だけ捲回体100の軸方向中央部100cに浸透する。
Here, the electrolytic solution E penetrates the central portion 100c in the axial direction of the wound body 100 by the same amount as the gas G is generated, that is, by the same amount as the volume of the gas G.
For example, when about 3 cc of gas G is generated during the initial charging step, the electrolyte E penetrates the axially central portion 100c of the wound body 100 by about 3 cc.

そこで、製造方法では、初期充電工程時に、体積が減少した後の捲回体内部空間S1の体積と同程度の量だけガスGが発生するように、量が調整された添加物LPFOを電解液Eに添加している。
また、電解液Eに対する添加物LPFOの添加量は、初期充電時におけるガスGの発生によって、初期充電終了時における外装30内の圧力が、大気圧と同程度となる量とすることができる。
Therefore, in the manufacturing method, the additive LPFO whose amount is adjusted so that the gas G is generated in an amount equivalent to the volume of the wound body internal space S1 after the volume is reduced during the initial charging step is used as the electrolytic solution. E is added.
Further, the amount of the additive LPFO added to the electrolytic solution E can be set to such an amount that the pressure in the exterior 30 at the end of the initial charging becomes approximately the same as the atmospheric pressure due to the generation of the gas G at the initial charging.

これにより、製造方法は、初期充電工程時に発生するガスGの量を減らして外装30内の圧力が必要以上に高くなることを抑制できる。   Thereby, the manufacturing method can suppress the quantity of the gas G generated at the time of an initial charge process, and can suppress that the pressure in the exterior 30 becomes higher than necessary.

従って、製造方法は、捲回体100の全面に均一な皮膜を形成できるとともに、後の工程でガス抜きを行うことなく電池10を製造できる。   Therefore, the manufacturing method can form a uniform film on the entire surface of the wound body 100 and can manufacture the battery 10 without degassing in a later step.

なお、製造方法では、減圧工程時に捲回体内部空間の空気の多くを外部に排出することが好ましい。
これにより、製造方法は、浸透工程でより多くの電解液を捲回体に浸透させることができるため、初期充電工程時に意図的に発生させるガスの量を減らすことができる。従って、製造方法は、初期充電工程時に外装内の圧力が高くなることを確実に防止できる。
In the manufacturing method, it is preferable that most of the air in the winding body inner space is discharged to the outside during the decompression step.
Thereby, since the manufacturing method can make more electrolyte solution osmose | permeate a winding body at an osmosis | permeation process, it can reduce the quantity of the gas deliberately generated at the time of an initial charge process. Therefore, the manufacturing method can reliably prevent the pressure in the exterior from increasing during the initial charging step.

また、浸透工程では、必ずしも捲回体外部空間と捲回体内部空間との圧力が平衡になるまで待機する必要はない。
本実施形態の製造方法は、捲回体外部空間Sと捲回体内部空間S1との圧力が平衡になるまで待機することで、加圧工程前に捲回体内部空間S1の体積をより小さくしている。
これにより、製造方法は、浸透工程でより多くの電解液を捲回体に浸透させることができるため、初期充電工程時に意図的に発生させるガスの量を減らすことができる。
In the infiltration step, it is not always necessary to wait until the pressures in the wound body outer space and the wound body inner space are balanced.
The manufacturing method of this embodiment waits until the pressure of the wound body outer space S and the wound body inner space S1 is in equilibrium, thereby reducing the volume of the wound body inner space S1 before the pressurizing step. doing.
Thereby, since the manufacturing method can make more electrolyte solution osmose | permeate a winding body at an osmosis | permeation process, it can reduce the quantity of the gas deliberately generated at the time of an initial charge process.

初期充電工程を行った後で、製造方法では、外装30(電池10)を高温エージングする高温エージング工程を行う。高温エージング工程は、初期充電工程時に外装30を拘束する拘束時具によって外装30を拘束したままの状態で、外装30の密閉状態を維持しつつ、高温環境下に外装30を一定時間放置する工程である。
これにより、製造方法では、二次電池10の放電特性を安定させる。
After performing the initial charging step, in the manufacturing method, a high temperature aging step of performing high temperature aging on the exterior 30 (battery 10) is performed. The high-temperature aging step is a step of leaving the exterior 30 for a certain period of time in a high-temperature environment while maintaining the sealed state of the exterior 30 while the exterior 30 is being restrained by a restraining tool that restrains the exterior 30 during the initial charging step. It is.
Thereby, in the manufacturing method, the discharge characteristics of the secondary battery 10 are stabilized.

高温エージング工程を行った後で、製造方法では、電圧の検査を行って、前記拘束治具による外装30の拘束を解除する。
製造方法では、このようにして電池10を製造する。
After performing the high temperature aging process, in the manufacturing method, the voltage is inspected and the restraint of the exterior 30 by the restraining jig is released.
In the manufacturing method, the battery 10 is manufactured in this way.

以上のように、電池10の電解液Eには、電池10が初期充電されるときに、体積が減少した後の捲回体内部空間S1の体積と同程度の量だけ添加物LPFOの分解反応によるガスGが発生するように、量が調整された添加物LPFOが添加される。   As described above, when the battery 10 is initially charged, the electrolytic solution E of the battery 10 decomposes the additive LPFO by an amount similar to the volume of the wound body internal space S1 after the volume is reduced. The additive LPFO whose amount is adjusted so as to generate the gas G is added.

ここで、製造方法は、捲回体100の形状、例えば、その軸方向の長さおよび厚み(巻き数)等によって、初期充電工程時だけでは皮膜を形成する時間が足りず、浸透工程後の捲回体内部空間S1の体積と同程度の量だけ初期充電工程時にガスGを発生させることができない可能性がある。
この場合には、高温エージング工程時に引き続き皮膜が形成される。従って、この場合、製造方法では、高温エージング工程時に残りのガスGを発生させることとなる。
つまり、この場合には、高温エージング工程時に捲回体100の軸方向中央部100cまで電解液Eが浸透し、その後、捲回体100の軸方向中央部100cに皮膜が形成されることとなる。
Here, in the manufacturing method, due to the shape of the wound body 100, for example, the length and thickness (the number of windings) in the axial direction, there is not enough time to form a film only at the time of the initial charging process. There is a possibility that the gas G cannot be generated during the initial charging step by an amount equivalent to the volume of the wound body internal space S1.
In this case, a film is continuously formed during the high temperature aging process. Accordingly, in this case, in the manufacturing method, the remaining gas G is generated during the high temperature aging process.
That is, in this case, the electrolytic solution E penetrates to the axial center part 100c of the wound body 100 during the high temperature aging process, and then a film is formed on the axial center part 100c of the wound body 100. .

具体的には、電解液Eの浸透は、高温エージング工程によって高温になり体積が膨張した捲回体外部空間S、および捲回体外部空間Sに存在するガスGの気泡が、電解液Eを捲回体100の軸方向中央部100cに押し込むことにより行われる。この場合、電池10の温度上昇によって、電解液E中に溶解していた気泡が外部へ出ていくため、電解液Eの捲回体100の軸方向中央部100cへの浸透が効果的に行われることとなる。   Specifically, the penetration of the electrolytic solution E is caused by the winding body outer space S whose volume is expanded by the high temperature aging process and the gas G bubbles existing in the winding body outer space S This is done by pushing into the central part 100c in the axial direction of the wound body 100. In this case, since the bubbles dissolved in the electrolytic solution E go out to the outside due to the temperature rise of the battery 10, the electrolytic solution E effectively permeates the axially central portion 100c of the wound body 100. Will be.

前述のように、高温エージング工程では、高温環境下に外装30が放置される。このため、外装30は、高温エージング工程時に一定の温度に加熱されることとなる。
従って、高温エージング工程において、捲回体外部空間Sおよび捲回体内部空間S1、すなわち、外装30内の圧力は上昇する。
As described above, in the high temperature aging process, the exterior 30 is left in a high temperature environment. For this reason, the exterior 30 is heated to a constant temperature during the high temperature aging process.
Therefore, in the high temperature aging process, the pressure inside the wound body outer space S and the wound body inner space S1, that is, the exterior 30 increases.

本実施形態の製造方法では、高温エージング工程時に外装30内の圧力が電解液Eの飽和蒸気圧以上となるように、添加物LPFOの量、すなわち、初期充電工程時におけるガスGの発生量を調整している。このように、電解液Eには、ガスGの発生によって、高温エージング工程時における外装30内の圧力が、電解液Eの高温エージング時における飽和蒸気圧以上に高くなる量の添加物LPFOが添加されている。   In the manufacturing method of the present embodiment, the amount of additive LPFO, that is, the amount of gas G generated in the initial charging step, is adjusted so that the pressure in the outer package 30 is equal to or higher than the saturated vapor pressure of the electrolyte E during the high temperature aging step. It is adjusted. As described above, the additive LPFO is added to the electrolytic solution E by the generation of the gas G so that the pressure in the exterior 30 during the high temperature aging process becomes higher than the saturated vapor pressure during the high temperature aging of the electrolytic solution E. Has been.

これによれば、製造方法は、高温エージング工程時に電解液Eが揮発することを防止できる。
従って、製造方法は、高温エージング工程時に揮発した電解液Eが捲回体100の軸方向中央部100cを満たしてしまうことを防止できる。つまり、製造方法は、揮発した電解液Eが液体の電解液Eの捲回体100への浸透を阻害してしまうことを防止できる。
According to this, the manufacturing method can prevent the electrolyte solution E from volatilizing during the high temperature aging process.
Therefore, the manufacturing method can prevent the electrolytic solution E volatilized during the high temperature aging process from filling the axially central portion 100c of the wound body 100. That is, the manufacturing method can prevent the volatilized electrolytic solution E from inhibiting the penetration of the liquid electrolytic solution E into the wound body 100.

このため、製造方法は、高温エージング工程でも、捲回体100の軸方向中央部100cに電解液Eを浸透させることができるとともに、捲回体100の軸方向中央部100cに皮膜を形成できる。
従って、製造方法は、捲回体100の形状に関わらず、確実に捲回体100に均一な皮膜を形成できる。
For this reason, in the manufacturing method, the electrolytic solution E can be permeated into the axially central portion 100c of the wound body 100 even in the high temperature aging process, and a film can be formed on the axially central portion 100c of the wound body 100.
Therefore, the manufacturing method can reliably form a uniform film on the wound body 100 regardless of the shape of the wound body 100.

また、製造方法では、電解液Eに添加する添加剤LPFOの量、すなわち、ガスGの発生量を調整し、高温エージング工程前(初期充電工程直後)に外装30内の圧力が電解液Eの飽和蒸気圧よりも低くなるようにしている。   Further, in the manufacturing method, the amount of additive LPFO added to the electrolytic solution E, that is, the amount of gas G generated is adjusted, and the pressure in the exterior 30 is adjusted to the level of the electrolytic solution E before the high temperature aging process (immediately after the initial charging process). It is designed to be lower than the saturated vapor pressure.

これにより、製造方法は、外装30内の圧力が必要以上に高くなってしまうことを防止できるため、後の工程でガス抜きを行うことなく電池10を製造できる。   Thereby, since the manufacturing method can prevent the pressure in the exterior 30 from becoming higher than necessary, the battery 10 can be manufactured without degassing in a later step.

このように、電解液Eには、ガスGの発生によって、高温エージング工程時に外装30内の圧力が電解液Eの飽和蒸気圧以上に高くなるとともに、初期充電工程直後における外装30内の圧力が電解液Eの飽和蒸気圧よりも低くなるように、量が調整された添加物LPFOが添加される。
このような添加物LPFOの量は、高温エージングの条件(外装30を加熱する温度)および初期充電工程直後の外装30内の圧力等に基づいて適宜設定される。
As described above, in the electrolytic solution E, due to the generation of the gas G, the pressure in the exterior 30 becomes higher than the saturated vapor pressure of the electrolytic solution E during the high temperature aging process, and the pressure in the exterior 30 immediately after the initial charging process is increased. The additive LPFO whose amount is adjusted so as to be lower than the saturated vapor pressure of the electrolytic solution E is added.
The amount of such additive LPFO is appropriately set based on the conditions for high-temperature aging (temperature for heating the exterior 30), the pressure in the exterior 30 immediately after the initial charging step, and the like.

ここで、初期充電工程時に発生するガスGは、ある電位領域において発生する。皮膜の形成速度は、初期充電工程時の充電レートが高くなるにつれて速くなる。   Here, the gas G generated during the initial charging process is generated in a certain potential region. The film formation rate increases as the charge rate during the initial charging step increases.

そこで、製造方法の初期充電工程では、ガスGが発生する電位領域において、他の電位領域よりも低レート、すなわち、電池10に低電流を流して電池10を充電する。
つまり、製造方法では、一定のレートで初期充電工程を行うのではなく、ガスGが発生する電位領域を低レート、他の電位領域を前記低レートよりも高いレートにして初期充電工程を行う。
Therefore, in the initial charging step of the manufacturing method, the battery 10 is charged by flowing a lower current in the potential region where the gas G is generated than the other potential regions, that is, by passing a low current through the battery 10.
That is, in the manufacturing method, the initial charging process is not performed at a constant rate, but the initial charging process is performed with the potential region where the gas G is generated at a low rate and the other potential regions at a higher rate than the low rate.

このようなガスGが発生する電位領域は、例えば、添加物の種類等によって異なっており、初期充電工程時に捲回体外部空間Sの圧力を市販の圧力センサで測定し、当該測定結果の中で圧力が上昇したときの電位領域を評価した結果等に基づいて予め確認される。   The potential region where such gas G is generated varies depending on, for example, the type of additive, and the pressure of the wound body external space S is measured with a commercially available pressure sensor during the initial charging process. This is confirmed in advance based on the result of evaluating the potential region when the pressure increases.

製造方法は、このようにして初期充電工程を行うことで、皮膜の形成速度を緩やかにして、皮膜の形成が電解液Eの捲回体100の軸方向中央部100cへの浸透に追いついてしまうことを確実に防止できる。また、製造方法は、捲回体100の軸方向中央部100cに十分に電解液Eを浸透させることができる。
従って、製造方法は、初期充電工程時(または、高温エージング時)に電解液Eを捲回体100の全面に浸透させてから、捲回体100の全面に皮膜を形成できる。
In the manufacturing method, by performing the initial charging step in this way, the formation speed of the film is reduced, and the formation of the film catches up with the penetration of the electrolytic solution E into the central portion 100c in the axial direction of the wound body 100. Can be surely prevented. Moreover, the manufacturing method can fully permeate | transmit the electrolyte solution E to the axial direction center part 100c of the winding body 100. FIG.
Therefore, the manufacturing method can form a film on the entire surface of the wound body 100 after the electrolyte E has penetrated the entire surface of the wound body 100 during the initial charging step (or during high-temperature aging).

つまり、製造方法は、高レートで充電した場合と比較して、より確実に捲回体100に均一な皮膜を形成できる。   That is, the manufacturing method can form a uniform film on the wound body 100 more reliably as compared with the case of charging at a high rate.

なお、製造方法では、ガスが発生する電位領域において、1C以下のレートで充電することが好ましい。特に、製造方法では、0.1C以下のレートで充電することが特に好ましい。
これにより、製造方法は、ガスの発生をより緩やかにすることができるため、より確実に捲回体に均一な皮膜を形成できる。
In the manufacturing method, it is preferable to charge at a rate of 1 C or less in a potential region where gas is generated. In particular, in the manufacturing method, it is particularly preferable to charge at a rate of 0.1 C or less.
Thereby, since the production method can make the gas generation more gradual, a uniform film can be more reliably formed on the wound body.

次に、電解液Eに添加する添加物の種類を変更して電池を製造し、各電池の皮膜を評価した結果について説明する。   Next, a description will be given of the results of manufacturing batteries by changing the type of additive added to the electrolytic solution E and evaluating the coating of each battery.

図11に示すように、皮膜の評価では、添加物として、本実施形態の添加物LPFOを採用して製造した本実施形態の電池10と、LiBOB(リチウムビスオキサラートボラート、以下に示す構造式2参照)を採用して製造した電池とを製造した。

Figure 0006066213
As shown in FIG. 11, in the evaluation of the film, the battery 10 of the present embodiment manufactured by adopting the additive LPFO of the present embodiment as an additive, and LiBOB (lithium bisoxalate borate, the structure shown below) A battery manufactured using the formula 2) was manufactured.
Figure 0006066213

添加物LiBOBは、皮膜形成時の分解反応で発生するガスの量が添加物LPFOよりも少ない添加物である。   The additive LiBOB is an additive in which the amount of gas generated by the decomposition reaction during film formation is less than that of the additive LPFO.

以下では、添加物LiBOBを採用して製造した電池を、「比較例の電池」と表記する。   Hereinafter, a battery manufactured using the additive LiBOB is referred to as a “battery of a comparative example”.

皮膜の評価では、添加物の種類が異なる点を除いて、同じ条件で各電池を製造した。   In the evaluation of the film, each battery was manufactured under the same conditions except that the types of additives were different.

皮膜の評価では、各電池を製造した後で、外装30を解体して捲回体100を取り出し、捲回体100に形成される皮膜の元素を分析することで、皮膜を評価した。   In the evaluation of the film, after each battery was manufactured, the outer package 30 was disassembled, the wound body 100 was taken out, and the elements of the film formed on the wound body 100 were analyzed to evaluate the film.

比較例の電池は、捲回体の軸方向中途部から多くの皮膜の元素が検出された。また、比較例の電池は、捲回体の軸方向中央部からあまり皮膜の元素が検出されなかった。
つまり、比較例の電池は、捲回体に均一な皮膜が形成されなかった。
In the battery of the comparative example, many elements of the film were detected from the middle in the axial direction of the wound body. Further, in the battery of the comparative example, the film element was not detected so much from the central portion in the axial direction of the wound body.
That is, in the battery of the comparative example, a uniform film was not formed on the wound body.

これは、初期充電工程時に添加物LiBOBの分解反応によって発生するガスの量が少ないため、捲回体の軸方向中央部まで電解液を浸透させることができなかったことによるものであると考えられる。   This is considered to be due to the fact that the amount of gas generated by the decomposition reaction of the additive LiBOB during the initial charging step is small, so that the electrolyte solution could not penetrate to the central portion in the axial direction of the wound body. .

一方、本実施形態の電池10は、比較例の電池と比較して、捲回体100の軸方向一端部から軸方向他端部まで均一に皮膜が形成されている。   On the other hand, as compared with the battery of the comparative example, the battery 10 of the present embodiment has a film uniformly formed from one axial end of the wound body 100 to the other axial end.

また、電解液Eに対する添加物としてLPFOを用いた電池10と、電解液Eに対する添加物としてLiBOBを用いた電池とについて、外装30内への電解液Eの注液後から、高温エージング終了時までの外装30内圧力の経時変化について確認したので説明する。   Moreover, about the battery 10 which used LPFO as an additive with respect to the electrolyte solution E, and the battery which used LiBOB as an additive with respect to the electrolyte solution E, after injection | pouring of the electrolyte solution E in the exterior 30, at the time of completion | finish of high temperature aging Since the change with time of the internal pressure of the exterior 30 was confirmed, explanation will be given.

図12に示すように、外装30内へ電解液を注液した後、外装30を密閉して放置すると、添加物LPFOの電池10および添加物LiBOBの電池の両方において、電解液の浸透とともに、外装30内圧力が減少した。
その後、初期充電を行うと、ガスGの発生量が少ない添加物LiBOBの電池においては、外装30内圧力の変化は殆ど見られなかったが、ガスGの発生量が多い添加物LPFOの電池10においては、外装30内圧力が大気圧まで復圧した。
As shown in FIG. 12, after injecting the electrolytic solution into the exterior 30, when the exterior 30 is sealed and left, in both the additive LPFO battery 10 and the additive LiBOB battery, the electrolyte solution penetrates. The pressure inside the exterior 30 decreased.
Thereafter, when the initial charge is performed, in the additive LiBOB battery with a small amount of gas G generated, almost no change in the pressure in the exterior 30 was observed, but the additive LPFO battery 10 with a large amount of gas G generated. , The pressure inside the exterior 30 was restored to atmospheric pressure.

さらに、高温エージングを開始すると、電池温度の上昇により外装30内圧力が上昇した。この場合、添加物LiBOBの電池においては、外装30内圧力が電解液Eの飽和蒸気圧よりも低い圧力となるため、高温エージング中に電解液Eが揮発し続けた。これにより、外装30内圧力は高温エージング中に上昇しつづけた。
一方、添加物LPFOの電池10においては、電池10の昇温により外装30内圧力が電解液Eの飽和蒸気圧以上に上昇した。従って、高温エージング中に電解液Eの揮発は発生しなかった。このように、添加物LPFOの電池10では、電解液Eの揮発を伴わずに外装30内圧力が上昇したため、電解液Eの浸透が促進され、捲回体100が全面的に均一に濡れた。
また、高温エージングが終了すると、添加物LPFOの電池10においては、外装30内圧力が減少し、大気圧に戻った。添加物LiBOBの電池においても、高温エージングの終了に伴い、外装30内圧力が減少した。
Furthermore, when high-temperature aging was started, the pressure in the exterior 30 increased due to an increase in battery temperature. In this case, in the battery of the additive LiBOB, the pressure inside the outer package 30 is lower than the saturated vapor pressure of the electrolytic solution E, and thus the electrolytic solution E continued to volatilize during high temperature aging. Thereby, the pressure in the exterior 30 continued to rise during high temperature aging.
On the other hand, in the battery 10 of the additive LPFO, the internal pressure of the exterior 30 increased to a value equal to or higher than the saturated vapor pressure of the electrolyte E as the battery 10 was heated. Therefore, volatilization of the electrolytic solution E did not occur during high temperature aging. As described above, in the battery 10 of the additive LPFO, the pressure inside the exterior 30 increased without volatilization of the electrolytic solution E, so that the penetration of the electrolytic solution E was promoted and the wound body 100 was uniformly wetted over the entire surface. .
Further, when the high temperature aging was completed, in the battery 10 of the additive LPFO, the pressure inside the exterior 30 decreased and returned to the atmospheric pressure. Also in the battery of additive LiBOB, the pressure in the exterior 30 decreased with the end of the high temperature aging.

以上より、製造方法では、ガスGが発生しやすい添加物(本実施形態では添加物LPFO)を電解液Eに添加することが好ましいことがわかる。   From the above, it can be seen that in the manufacturing method, it is preferable to add an additive that easily generates gas G (additive LPFO in the present embodiment) to the electrolytic solution E.

なお、製造方法では、皮膜形成時の分解反応で多くのガスが発生する添加物であればよく、本実施形態のような添加物LPFOに限定されるものでない。例えば、皮膜形成時の分解反応でガスが発生する添加物として、ビニリデンカーボネートを用いることもできる。   Note that the manufacturing method is not limited to the additive LPFO as in the present embodiment as long as it is an additive that generates a large amount of gas in the decomposition reaction during film formation. For example, vinylidene carbonate can also be used as an additive that generates gas in the decomposition reaction during film formation.

10 電池(二次電池)
30 外装(電池ケース)
100 捲回体
100a・100b 軸方向両端部
E 電解液
LPFO 添加物
S 捲回体外部空間
S1 捲回体内部空間
10 Battery (secondary battery)
30 Exterior (battery case)
100 Winding body 100a / 100b Both ends in the axial direction E Electrolyte LPFO additive S Winding body outer space S1 Winding body inner space

Claims (5)

電池ケースと捲回体と電解液とを備える密閉型の二次電池の製造方法であって、
前記電池ケースの下面に対して捲回軸方向が平行となるようにして前記捲回体が収納された状態の前記電池ケース内を減圧する工程と、
減圧した前記電池ケース内に、分解反応によりガスを発生し得る添加物を添加した電解液を注液する工程と、
前記電解液を注液した前記電池ケースを密閉する工程と、
密閉した前記電池ケースと捲回体との間の空間である捲回体外部空間と、前記捲回体内部空間との差圧を小さくするために待機して、前記捲回体の軸方向両端部から前記電解液を浸透させて前記捲回体内部空間の体積を減少させる工程と、
前記捲回体に前記電解液を浸透させた二次電池を初期充電する工程と、
前記電池ケースの密閉を維持しつつ、前記初期充電した前記二次電池を高温エージングする工程と、
を行い、
前記電解液には、
前記添加物の分解反応によるガスの発生によって、前記高温エージングする工程を行うときの前記電池ケース内の圧力が、前記電解液の高温エージング時における飽和蒸気圧以上に高くなる量の添加物が添加される、
密閉型二次電池の製造方法。
A method for producing a sealed secondary battery comprising a battery case, a wound body and an electrolyte,
Depressurizing the inside of the battery case in a state in which the wound body is housed so that the winding axis direction is parallel to the lower surface of the battery case;
Injecting an electrolytic solution to which an additive capable of generating a gas by a decomposition reaction is added into the decompressed battery case;
Sealing the battery case filled with the electrolytic solution;
Both ends of the wound body in the axial direction are on standby to reduce the differential pressure between the wound body outer space, which is a space between the battery case and the wound body, and the inner space of the wound body. Infiltrating the electrolyte solution from the portion to reduce the volume of the winding body internal space; and
A step of initially charging a secondary battery in which the electrolytic solution is infiltrated into the wound body;
Maintaining the sealed battery case while aging the initially charged secondary battery at a high temperature;
And
The electrolyte includes
Due to the generation of gas due to the decomposition reaction of the additive, an amount of additive is added such that the pressure in the battery case when performing the high-temperature aging step is higher than the saturated vapor pressure during high-temperature aging of the electrolyte. To be
A manufacturing method of a sealed secondary battery.
前記電解液には、
前記ガスの発生によって、前記高温エージングする工程を行うときの前記電池ケース内の圧力が、前記電解液の高温エージング時における飽和蒸気圧以上に高くなるように量が調整されるとともに、
前記初期充電する工程において前記電池ケース内の圧力が前記電解液の高温エージング時における飽和蒸気圧よりも低くなる量の前記添加物が添加される、
請求項1に記載の二次電池の製造方法。
The electrolyte includes
The amount of the gas is adjusted so that the pressure in the battery case when performing the high temperature aging step is higher than the saturated vapor pressure at the time of high temperature aging of the electrolyte by the generation of the gas,
In the initial charging step, an amount of the additive is added such that the pressure in the battery case is lower than the saturated vapor pressure during high-temperature aging of the electrolyte.
The manufacturing method of the secondary battery of Claim 1.
前記電解液には、
前記ガスの発生によって、前記初期充電終了時における前記電池ケース内の圧力が、大気圧と同程度となる量の前記添加物が添加される、
請求項1または請求項2に記載の二次電池の製造方法。
The electrolyte includes
Due to the generation of the gas, the amount of the additive is added such that the pressure in the battery case at the end of the initial charge is approximately the same as the atmospheric pressure.
The manufacturing method of the secondary battery of Claim 1 or Claim 2.
前記初期充電する工程では、
前記ガスが発生する電位領域において、他の電位領域よりも低レートで前記二次電池を充電する、
請求項1〜請求項3の何れか一項に記載の二次電池の製造方法。
In the initial charging step,
In the potential region where the gas is generated, the secondary battery is charged at a lower rate than other potential regions.
The manufacturing method of the secondary battery as described in any one of Claims 1-3.
電池ケースと
記電池ケースに収納された捲回体であって前記電池ケースの下面に対して捲回軸方向が平行である捲回体と、電解液と、を具備した密閉型の二次電池であって、
記電解液には、分解反応によりガスを発生し得る添加物が添加されており、
前記添加物の添加量は、以下の条件:
該添加物の分解反応によるガスの発生によって、高温エージングを行うときの密閉された前記電池ケース内の圧力が、前記電解液の高温エージング時における飽和蒸気圧以上に高くなる
を満たす量であることを特徴とする密閉型二次電池。
A battery case ,
In the secondary battery of the previous SL and the wound body is parallel winding axis direction with respect to the lower surface of the battery case a wound body which is housed in the battery case, the hermetic equipped with an electrolytic solution, a There,
The front Symbol electrolyte, additives capable of generating gas by decomposition reactions are added,
The amount of the additive added is as follows:
By the generation of gas due to the decomposition reaction of the additive, sealed pressure in the battery case when performing Atsushi Ko aging is higher on the saturated vapor pressure at high temperature aging of the electrolyte;
A sealed secondary battery, characterized in that the amount satisfies the above .
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